AU4582189A - Argon purification - Google Patents
Argon purificationInfo
- Publication number
- AU4582189A AU4582189A AU45821/89A AU4582189A AU4582189A AU 4582189 A AU4582189 A AU 4582189A AU 45821/89 A AU45821/89 A AU 45821/89A AU 4582189 A AU4582189 A AU 4582189A AU 4582189 A AU4582189 A AU 4582189A
- Authority
- AU
- Australia
- Prior art keywords
- ppm
- oxygen
- rectification
- argon
- argon purification
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 title abstract 6
- 229910052786 argon Inorganic materials 0.000 title abstract 3
- 238000000746 purification Methods 0.000 title 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 2
- 239000001301 oxygen Substances 0.000 abstract 2
- 229910052760 oxygen Inorganic materials 0.000 abstract 2
- 238000000926 separation method Methods 0.000 abstract 2
- 238000000034 method Methods 0.000 abstract 1
- 238000012856 packing Methods 0.000 abstract 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04248—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion
- F25J3/04284—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
- F25J3/0429—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams of feed air, e.g. used as waste or product air or expanded into an auxiliary column
- F25J3/04303—Lachmann expansion, i.e. expanded into oxygen producing or low pressure column
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04406—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system
- F25J3/04412—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04654—Producing crude argon in a crude argon column
- F25J3/04666—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system
- F25J3/04672—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser
- F25J3/04678—Producing crude argon in a crude argon column as a parallel working rectification column of the low pressure column in a dual pressure main column system having a top condenser cooled by oxygen enriched liquid from high pressure column bottoms
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04642—Recovering noble gases from air
- F25J3/04648—Recovering noble gases from air argon
- F25J3/04721—Producing pure argon, e.g. recovered from a crude argon column
- F25J3/04727—Producing pure argon, e.g. recovered from a crude argon column using an auxiliary pure argon column for nitrogen rejection
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/90—Details relating to column internals, e.g. structured packing, gas or liquid distribution
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2235/00—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
- F25J2235/58—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being argon or crude argon
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2250/00—Details related to the use of reboiler-condensers
- F25J2250/30—External or auxiliary boiler-condenser in general, e.g. without a specified fluid or one fluid is not a primary air component or an intermediate fluid
- F25J2250/42—One fluid being nitrogen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2250/00—Details related to the use of reboiler-condensers
- F25J2250/30—External or auxiliary boiler-condenser in general, e.g. without a specified fluid or one fluid is not a primary air component or an intermediate fluid
- F25J2250/58—One fluid being argon or crude argon
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/12—Particular process parameters like pressure, temperature, ratios
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S62/00—Refrigeration
- Y10S62/923—Inert gas
- Y10S62/924—Argon
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S62/00—Refrigeration
- Y10S62/939—Partial feed stream expansion, air
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Removal Of Specific Substances (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Motor Or Generator Cooling System (AREA)
- Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
Abstract
A process and apparatus for air separation by low temperature rectification are described in which argon is obtained exclusively by rectification. A crude argon column (24) is equipped with at least 150 theoretical plates in the form of low pressure drop packing so that, in it, a substantially complete separation of the oxygen is possible, e.g., less than about 10 ppm, preferably less than 1 ppm oxygen.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3840506 | 1988-12-01 | ||
DE3840506A DE3840506A1 (en) | 1988-12-01 | 1988-12-01 | METHOD AND DEVICE FOR AIR DISASSEMBLY |
Publications (2)
Publication Number | Publication Date |
---|---|
AU4582189A true AU4582189A (en) | 1990-06-07 |
AU617226B2 AU617226B2 (en) | 1991-11-21 |
Family
ID=6368245
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU45821/89A Expired AU617226B2 (en) | 1988-12-01 | 1989-12-01 | Argon purification |
Country Status (11)
Country | Link |
---|---|
US (1) | US5019145A (en) |
EP (1) | EP0377117B2 (en) |
JP (1) | JPH0781781B2 (en) |
KR (1) | KR950014009B1 (en) |
CN (1) | CN1019690B (en) |
AT (1) | ATE74199T1 (en) |
AU (1) | AU617226B2 (en) |
CA (1) | CA2004263C (en) |
DE (2) | DE3840506A1 (en) |
ES (1) | ES2031677T5 (en) |
ZA (1) | ZA899186B (en) |
Families Citing this family (60)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4983194A (en) * | 1990-02-02 | 1991-01-08 | Air Products And Chemicals, Inc. | Production of high purity argon |
US4994098A (en) * | 1990-02-02 | 1991-02-19 | Air Products And Chemicals, Inc. | Production of oxygen-lean argon from air |
US5133790A (en) * | 1991-06-24 | 1992-07-28 | Union Carbide Industrial Gases Technology Corporation | Cryogenic rectification method for producing refined argon |
US5161380A (en) * | 1991-08-12 | 1992-11-10 | Union Carbide Industrial Gases Technology Corporation | Cryogenic rectification system for enhanced argon production |
US5235816A (en) * | 1991-10-10 | 1993-08-17 | Praxair Technology, Inc. | Cryogenic rectification system for producing high purity oxygen |
US5207066A (en) * | 1991-10-22 | 1993-05-04 | Bova Vitaly I | Method of air separation |
US5237823A (en) * | 1992-03-31 | 1993-08-24 | Praxair Technology, Inc. | Cryogenic air separation using random packing |
JP2966999B2 (en) * | 1992-04-13 | 1999-10-25 | 日本エア・リキード株式会社 | Ultra high purity nitrogen / oxygen production equipment |
US5230217A (en) * | 1992-05-19 | 1993-07-27 | Air Products And Chemicals, Inc. | Inter-column heat integration for multi-column distillation system |
US5305611A (en) * | 1992-10-23 | 1994-04-26 | Praxair Technology, Inc. | Cryogenic rectification system with thermally integrated argon column |
US5311744A (en) * | 1992-12-16 | 1994-05-17 | The Boc Group, Inc. | Cryogenic air separation process and apparatus |
DE4317916A1 (en) * | 1993-05-28 | 1994-12-01 | Linde Ag | Process and apparatus for the isolation of argon |
DE4332870C2 (en) * | 1993-09-27 | 2003-02-20 | Linde Ag | Method and device for obtaining a krypton / xenon concentrate by low-temperature separation of air |
CA2142317A1 (en) * | 1994-02-24 | 1995-08-25 | Anton Moll | Process and apparatus for the recovery of pure argon |
DE4406049A1 (en) * | 1994-02-24 | 1995-09-07 | Linde Ag | Fractional distillation system for pure argon from air |
CA2142318A1 (en) * | 1994-02-24 | 1995-08-25 | Horst Corduan | Process and apparatus for recovery of pure argon |
DE4406069A1 (en) * | 1994-02-24 | 1995-09-07 | Linde Ag | Fractional distillation system for pure argon from air |
DE4406051A1 (en) * | 1994-02-24 | 1995-08-31 | Linde Ag | Fractional distillation of argon from air, with increased purity and economy, |
US5396772A (en) * | 1994-03-11 | 1995-03-14 | The Boc Group, Inc. | Atmospheric gas separation method |
GB9410696D0 (en) | 1994-05-27 | 1994-07-13 | Boc Group Plc | Air separation |
GB9412182D0 (en) * | 1994-06-17 | 1994-08-10 | Boc Group Plc | Air separation |
US5440884A (en) * | 1994-07-14 | 1995-08-15 | Praxair Technology, Inc. | Cryogenic air separation system with liquid air stripping |
GB9423955D0 (en) | 1994-11-24 | 1995-01-11 | Boc Group Plc | Air seperation |
DE4443190A1 (en) * | 1994-12-05 | 1996-06-13 | Linde Ag | Method and apparatus for the cryogenic separation of air |
GB9500514D0 (en) * | 1995-01-11 | 1995-03-01 | Boc Group Plc | Air separation |
GB9505645D0 (en) * | 1995-03-21 | 1995-05-10 | Boc Group Plc | Air separation |
US5557951A (en) * | 1995-03-24 | 1996-09-24 | Praxair Technology, Inc. | Process and apparatus for recovery and purification of argon from a cryogenic air separation unit |
JP3935503B2 (en) * | 1995-06-20 | 2007-06-27 | 大陽日酸株式会社 | Argon separation method and apparatus |
GB9513765D0 (en) * | 1995-07-06 | 1995-09-06 | Boc Group Plc | Production of argon |
DE19537913A1 (en) * | 1995-10-11 | 1997-04-17 | Linde Ag | Triple column process for the low temperature separation of air |
DE19543395A1 (en) | 1995-11-21 | 1997-05-22 | Linde Ag | Double column process and device for the low temperature separation of air |
DE19543953C1 (en) | 1995-11-25 | 1996-12-19 | Linde Ag | Recovery of oxygen@ and nitrogen@ under super-atmospheric pressure |
US5799508A (en) * | 1996-03-21 | 1998-09-01 | Praxair Technology, Inc. | Cryogenic air separation system with split kettle liquid |
FR2757421B1 (en) * | 1996-12-24 | 1999-01-15 | Air Liquide | PROCESS FOR PURIFYING CRYOGENIC FLUID BY FILTRATION AND / OR ADSORPTION |
US5768914A (en) * | 1997-07-28 | 1998-06-23 | Air Products And Chemicals, Inc. | Process to produce oxygen and argon using divided argon column |
US5916261A (en) * | 1998-04-02 | 1999-06-29 | Praxair Technology, Inc. | Cryogenic argon production system with thermally integrated stripping column |
US6347534B1 (en) * | 1999-05-25 | 2002-02-19 | Air Liquide Process And Construction | Cryogenic distillation system for air separation |
US6276170B1 (en) * | 1999-05-25 | 2001-08-21 | Air Liquide Process And Construction | Cryogenic distillation system for air separation |
DE19957017A1 (en) * | 1999-11-26 | 2001-05-31 | Linde Ag | Device for the production of argon |
US6321567B1 (en) | 2000-10-06 | 2001-11-27 | Praxair Technology, Inc. | Structured packing system for reduced distillation column height |
DE10153252A1 (en) * | 2001-10-31 | 2003-05-15 | Linde Ag | Process for recovering krypton and/or xenon by low temperature decomposition of air, comprises passing compressed purified process air to a rectifier system, removing a fraction containing krypton and xenon, and further processing |
US7087804B2 (en) * | 2003-06-19 | 2006-08-08 | Chevron U.S.A. Inc. | Use of waste nitrogen from air separation units for blanketing cargo and ballast tanks |
DE102007035619A1 (en) | 2007-07-30 | 2009-02-05 | Linde Ag | Process and apparatus for recovering argon by cryogenic separation of air |
EP2026024A1 (en) | 2007-07-30 | 2009-02-18 | Linde Aktiengesellschaft | Process and device for producing argon by cryogenic separation of air |
JP5642923B2 (en) * | 2008-06-10 | 2014-12-17 | エア・ウォーター株式会社 | Air separation method |
EP2211131A1 (en) | 2009-01-21 | 2010-07-28 | Linde AG | Method for operating an air segmentation assembly |
DE102009016043A1 (en) | 2009-04-02 | 2010-10-07 | Linde Ag | Method for operating a pure argon column, comprises initiating a nitrogen-containing argon stream into an upper- or middle area of the pure argon column from which lower area of the argon column is drawn-off to a pure argon product |
US8899075B2 (en) | 2010-11-18 | 2014-12-02 | Praxair Technology, Inc. | Air separation method and apparatus |
EP2645031A1 (en) | 2012-03-29 | 2013-10-02 | Linde Aktiengesellschaft | Separating column for a low temperature air separator facility, low temperature air separator facility and method for low temperature separation of air |
DE102012006484A1 (en) | 2012-03-29 | 2013-10-02 | Linde Aktiengesellschaft | Transportable package with a coldbox and method of manufacturing a cryogenic air separation plant |
DE102012006479A1 (en) | 2012-03-29 | 2013-10-02 | Linde Ag | Transportable package with a coldbox and method of manufacturing a cryogenic air separation plant |
DE102012008415A1 (en) | 2012-04-27 | 2013-10-31 | Linde Aktiengesellschaft | Transportable package comprising a cold box, cryogenic air separation plant and method of manufacturing a cryogenic air separation plant |
RU2659698C2 (en) | 2013-03-06 | 2018-07-03 | Линде Акциенгезелльшафт | Air separation plant, method for obtaining product containing argon, and method for manufacturing air separation plant |
CN103267403B (en) * | 2013-05-15 | 2015-09-16 | 兖矿集团有限公司 | A kind of system and method improving liquid argon yield |
CN103256081B (en) * | 2013-05-22 | 2015-04-22 | 南京飓能电控自动化设备制造有限公司 | Energy comprehensive utilization method based on supercritical air |
DE102013018664A1 (en) | 2013-10-25 | 2015-04-30 | Linde Aktiengesellschaft | Process for the cryogenic separation of air and cryogenic air separation plant |
EP3040665A1 (en) | 2014-12-30 | 2016-07-06 | Linde Aktiengesellschaft | Distillation system and plant for the production of oxygen by crygenic separation of air |
EP3048401A1 (en) | 2015-01-20 | 2016-07-27 | Linde Aktiengesellschaft | Method and device for variable extraction of argon by cryogenic separation of air |
US10663222B2 (en) * | 2018-04-25 | 2020-05-26 | Praxair Technology, Inc. | System and method for enhanced recovery of argon and oxygen from a nitrogen producing cryogenic air separation unit |
US11828532B2 (en) * | 2020-12-31 | 2023-11-28 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Method and apparatus for transfer of liquid |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE821951C (en) * | 1949-06-20 | 1951-11-22 | Linde Eismasch Ag | Process for the extraction of argon |
NL102363C (en) * | 1953-11-12 | |||
IT1034545B (en) * | 1975-03-26 | 1979-10-10 | Siad | PROCESS AND PLANT FOR OBTAINING THE ARGON STARTING FROM AN AIR FRACTION PROCESS |
IT1034544B (en) * | 1975-03-26 | 1979-10-10 | Siad | PROCEDURE AND PLANT FOR AIR FRACTION WITH A SIMPLE GRINDING COLUMN |
CH617357A5 (en) * | 1977-05-12 | 1980-05-30 | Sulzer Ag | |
DE3428968A1 (en) * | 1984-08-06 | 1986-02-13 | Linde Ag, 6200 Wiesbaden | METHOD AND DEVICE FOR DISASSEMBLING ROHARGON |
DE3436897A1 (en) * | 1984-10-08 | 1986-04-10 | Linde Ag, 6200 Wiesbaden | Process and apparatus for operating an air separation plant |
LU86284A1 (en) * | 1986-01-30 | 1987-09-03 | Belge Etat | PROCESS FOR OBTAINING ETHYLENE FROM ETHANOL |
US4871382A (en) * | 1987-12-14 | 1989-10-03 | Air Products And Chemicals, Inc. | Air separation process using packed columns for oxygen and argon recovery |
US4836836A (en) * | 1987-12-14 | 1989-06-06 | Air Products And Chemicals, Inc. | Separating argon/oxygen mixtures using a structured packing |
US4838913A (en) * | 1988-02-10 | 1989-06-13 | Union Carbide Corporation | Double column air separation process with hybrid upper column |
-
1988
- 1988-12-01 DE DE3840506A patent/DE3840506A1/en active Granted
-
1989
- 1989-11-29 CN CN89108846A patent/CN1019690B/en not_active Expired
- 1989-11-29 AT AT89122047T patent/ATE74199T1/en not_active IP Right Cessation
- 1989-11-29 DE DE8989122047T patent/DE58901041D1/en not_active Expired - Lifetime
- 1989-11-29 EP EP89122047A patent/EP0377117B2/en not_active Expired - Lifetime
- 1989-11-29 JP JP1310473A patent/JPH0781781B2/en not_active Expired - Lifetime
- 1989-11-29 ES ES89122047T patent/ES2031677T5/en not_active Expired - Lifetime
- 1989-11-30 CA CA002004263A patent/CA2004263C/en not_active Expired - Lifetime
- 1989-11-30 US US07/443,529 patent/US5019145A/en not_active Expired - Lifetime
- 1989-12-01 KR KR1019890017731A patent/KR950014009B1/en not_active IP Right Cessation
- 1989-12-01 ZA ZA899186A patent/ZA899186B/en unknown
- 1989-12-01 AU AU45821/89A patent/AU617226B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE3840506A1 (en) | 1990-06-07 |
DE58901041D1 (en) | 1992-04-30 |
KR900009433A (en) | 1990-07-04 |
CN1043196A (en) | 1990-06-20 |
ES2031677T3 (en) | 1992-12-16 |
EP0377117B2 (en) | 1995-05-17 |
ES2031677T5 (en) | 1995-09-16 |
US5019145A (en) | 1991-05-28 |
CA2004263A1 (en) | 1990-06-01 |
CN1019690B (en) | 1992-12-30 |
EP0377117A1 (en) | 1990-07-11 |
ATE74199T1 (en) | 1992-04-15 |
AU617226B2 (en) | 1991-11-21 |
KR950014009B1 (en) | 1995-11-20 |
ZA899186B (en) | 1990-08-29 |
EP0377117B1 (en) | 1992-03-25 |
JPH02247484A (en) | 1990-10-03 |
JPH0781781B2 (en) | 1995-09-06 |
CA2004263C (en) | 1994-02-01 |
DE3840506C2 (en) | 1992-01-16 |
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